EP0264268A2 - Wasserabweisende anorganische Produkte - Google Patents

Wasserabweisende anorganische Produkte Download PDF

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Publication number
EP0264268A2
EP0264268A2 EP87309066A EP87309066A EP0264268A2 EP 0264268 A2 EP0264268 A2 EP 0264268A2 EP 87309066 A EP87309066 A EP 87309066A EP 87309066 A EP87309066 A EP 87309066A EP 0264268 A2 EP0264268 A2 EP 0264268A2
Authority
EP
European Patent Office
Prior art keywords
cavities
range
silylating agent
inorganic
diameters
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP87309066A
Other languages
English (en)
French (fr)
Other versions
EP0264268A3 (en
EP0264268B1 (de
Inventor
Abraham Dr. Araya
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Unilever PLC
Original Assignee
Unilever PLC
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Unilever PLC filed Critical Unilever PLC
Priority to AT87309066T priority Critical patent/ATE76633T1/de
Publication of EP0264268A2 publication Critical patent/EP0264268A2/de
Publication of EP0264268A3 publication Critical patent/EP0264268A3/en
Application granted granted Critical
Publication of EP0264268B1 publication Critical patent/EP0264268B1/de
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B38/00Porous mortars, concrete, artificial stone or ceramic ware; Preparation thereof
    • C04B38/0022Porous mortars, concrete, artificial stone or ceramic ware; Preparation thereof obtained by a chemical conversion or reaction other than those relating to the setting or hardening of cement-like material or to the formation of a sol or a gel, e.g. by carbonising or pyrolysing preformed cellular materials based on polymers, organo-metallic or organo-silicon precursors
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2111/00Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
    • C04B2111/20Resistance against chemical, physical or biological attack
    • C04B2111/27Water resistance, i.e. waterproof or water-repellent materials

Definitions

  • This invention relates to a new hydrophobic, highly porous, three-dimensional, inorganic structure having a myriad of cavities interconnected by holes.
  • a three dimensional hydrophobic substantially inorganic porous structure comprising a myriad of cavities interconnected by holes in which the diameters of cavities are in the range of from 0.5 to 100 ⁇ m and the diameters of the holes are in the range of from 0.1 to 20 ⁇ m, the porosity of the structure having a narrow pore size distribution with the cavities having a pore volume of at least 2cc/g for a predetermined 10 ⁇ m range of sizes.
  • the diameters of the cavities are in the range of from to 0.5 to 50 ⁇ m, the diameters of the holes are in the range of from 0.5 to 10 ⁇ m and the cavities have a pore volume of at least 2cc/g for cavities having diameter within the range 0.5 to 10 ⁇ m. More preferably the diameters of the cavities are in the range of from 1 to 50 ⁇ m, the diameters of the holes are in the range of from 1 to 10 ⁇ m and the cavities have a pore volume of at least 2cc/g for cavities having diameters within the range l to 10 ⁇ m.
  • hydrophobic inorganic porous structures having a narrow pore size distribution can allow their employment in specific end users.
  • the proportion of cavities having a pore volume in the predetermined range of sizes can amount to at least 90% v/v with respect to the sum total of the cavity pore volume present.
  • the cavities can for example have a pore volume of up to 8cc/g for the said predertermined range of pore sizes.
  • Porosity of the structures can be measured by mercury porosimetry.
  • the inorganic material comprising the structure can be selected from the group comprising alumina, silica, titania, zirconia and mixtures thereof.
  • the structure is preferably rendered hydrophobic by the use of a silylating agent.
  • the silylating agent replaces the equivalent of at least 5 molar percent available hydroxy groups in the inorganic structure.
  • An upper limit to the level of silylating agent may be determined by the make-up at the structure, but can be the equivalent of up to 40 molar per cent available hydroxy groups in the inorganic structure.
  • silylating agent employed is suitably selected from the group comprising siloxanes, silazanes, oxysilanes, alkylhalosilanes, arylhalosilanes, alkyhalo-oxysilanes, arylhalo-oxysilanes, substituted derivatives and mixtures thereof.
  • the silylating agent selected and its amount will depend on the system required and the degree of hydrophobicity desired.
  • the present structures can however have a carbon content within the range 0.5 to 10% by weight with respect to the total weight of the structure. The actual proportion of carbon present will depend not only on the molar proportion of silylating groups present, but also their carbon chain length.
  • the present invention there is provided a process for preparing a three-dimensional hydrophobic substantially inorganic structure according to the first aspect of the present invention, the process comprising:
  • the inorganic structure is an inorganic oxide selected from alumina, silica, titania, zirconia and mixtures thereof.
  • the amount of silylating agent employed is preferably effective to replace the equivalent of at least 5 molar percent available hydroxy groups and up to the equivalent of 40 molar percent available hydroxy groups.
  • the aqueous solution of the precursors of the inorganic structure is contacted with an effective amount of a reactive silylating agent.
  • the precursors are for example appropriate inorganic salts and lower oxides suitable for forming the desired inorganic structure.
  • Contact between the precursors and the silylating agent thus occurs prior to causing the emulsion to set or gel.
  • Contact with the silylating agent in such a manner can for a given structure lead to a higher degree of silylating agent being incorporated than contacting the ready formed structure with a silylating agent.
  • the "oil" phase in the emulsion by which is meant a water-immiscible fluid, consists at least partially of the silylating agent employed.
  • the silylating agent can constitute the entirety of the "oil" phase or it can be diluted by use of or dissolved in an appropriate water-immiscible solvent, for example cyclohexane.
  • the silylating agent can thus be solid or liquid.
  • the ratio of silylating agent to solvent employed will depend on both the degree of hydrophobicity and the overall porosity of the structure required.
  • the amount of silylating agent is preferably between 2 and 50% by weight with respect to the weight of the emulsion.
  • porous inorganic structures can be provided which are hydrophobic both on the exterior surface and on the internal cavities and pores, providing sufficient silylating agent is employed.
  • Suitable reactive silylating agents for use in the present process are essentially those which are not hydrolysed or otherwise deactivated in the process. Likewise, the silylating agents should not, under the conditions of the process, trigger premature gelation of the inorganic material.
  • the reactive silylating agent is selected from the group comprising siloxanes, silazanes, oxysilanes, alkylhalosilates, arylhalosilanes and alkylhalo-oxysilanes, arylhalo-oxysilanes, substituted derivatives and mixtures thereof.
  • Suitable silanes include:
  • R-Si-0-Si-R and R-Si-NH-Si-R where R is -CH3 or -C2H5; and R′-Si-X m where R′ is -C n H 2n+1′ is l to 22) or -C6H5, m is 1 to 3 and -X is -Cl, -Br, -I, -OMe, -OEt.
  • the water­immiscible fluid, together with any unreacted silylating agent is removed from the structure and, optionally, any electrolytes can be washed out and the structure dried.
  • 0.05 g of 106-250 ⁇ particle size of the dried product was placed on the surface of 15 mls water in 100 ml beaker. Methanol was titrated onto the sample in small amounts. The beaker was shaken between additions of methanol. 28 mls of methanol were required for all the sample to be completely wetted and descend to the bottom of the beaker. A sample with similar particle size but made without the addition of any HMDS in the dispersed phase required less than 1 ml methanol to be completely wetted and sent to the bottom of the beaker.
  • Example 1 The procedure of Example 1 was repeated except that 114 mls of cyclohexane and 30 mls of HMDS were used.
  • the dried product had a pore volume of 4.4 cc/g between 1 to 10 ⁇ m and a carbon content of 2.7%.
  • SEM of the product showed a three-dimensional network structure with cavities interconnected by holes as shown in Figure 2 of the accompanying drawings.
  • Example 1 The procedure of Example 1 was repeated excepted that 72 mls of cyclohexane and 72 mls of HMDS were used.
  • the pore volume of the dried product between 1 to 10 ⁇ m was 4.3 cc/g and the carbon content was 6.5%.
  • 36 mls of methanol was required to wet and sink completely 0.05 g of 106-250 ⁇ particle size of the product to the bottom of a beaker containing 15 mls of water.
  • Scanning electron microscopy (SEM) of the product showed a three-dimensional network structure with cavities interconnected by holes.
  • Figure 1 is a porosity trace of the product of Example 3 which is a graph of cumulative pore volume in cc/g on the ordinate and pore diameter in log scale in microns on the abscicca.
  • Example 1 The procedure of Example 1 was repeated except that 36 mls of cyclohexane and 108 mls of HMDS were used.
  • the dried product had a pore volume of 4 cc/g between 1 to 10 ⁇ m and a carbon content of 9.1%.
  • SEM of the product showed a three-dimensional network structure with cavities interconnected by holes.
  • Example 1 The procedure of Example 1 was repeated except that 144 mls of HMDS was used.
  • the dried product had a pore volume of 3.7 cc/g between 1 to 10um and a carbon content of 9.8%.
  • SEM of the product showed a three-dimensional network structure with cavities interconnected by holes as shown in Figure 3 of the accompanying drawings.
  • the pore volume of the dried product was 3.4cc/g between 1 and 10 ⁇ m.
  • the product had an overall porosity of 4.93 cc/g and contained 13.6wt% carbon.
  • Example 6 The procedure of Example 6 was followed employing 63g sodium silicate solution (20% Si02), 0.6g Miranol, 0.52g Crodateric C, 141 mls cyclohexane and 3mls HMDS.
  • the product had an overall porosity of 5.78cc/g and a porosity between 0.5 and 5 ⁇ m of 5.23cc/g.
  • the carbon content of the product was 1.6 wt.%.
  • Example 6 The procedure of Example 6 was followed employing 63g of aqueous solution of sodium silicate (20% Si02), 0.63g Miranol, 0.52g Crodateric C, 138mls cyclohexane and 6mls HMDS.
  • the product had an overall porosity of 5.28cc/g and a porosity between 0.5 and 5 ⁇ m of 3.3cc/g and a carbon content of 2.65 wt.%.
  • Example 6 The procedure of Example 6 was followed employing 160g aqueous sodium silicate solution (containing 20% by weight SiO2), 1.6g Miranol, 1.3g Crodateric C, 348mls cyclohexane and 18mls HMDS.
  • the product had an overall porosity of 5.19cc/g and a porosity between 0.5 and 5 ⁇ m of 3cc/g.
  • the product contained 8.08 wt% carbon.
  • the product had an overall porosity of 6.08cc/g and a pore volume between 1 and 10 ⁇ m of 3.9cc/g.
  • the product contained 6.7wt% carbon.
  • sodium aluminosilicate sol prepared by mixing 53g acid alum [2.76% Al2O3, 20% H and 77.24% H2O] and 165g sodium silicate [10.4% SiO2 by weight]
  • aluminosilicate sol prepared by mixing 53g acid alum [2.76% Al2O3, 20% H and 77.24% H2O] and 165g sodium silicate [10.4% SiO2 by weight]
  • 130mls cyclohexane were added to the aluminosilicate/ emulsifying agent mixture followed by 14mls HMDS.
  • the mixture was stirred using a vibro mixer for 10 minutes and the resulting emulsion was left to stand for 15 minutes.
  • the emulsion was gelled by dropping into 1M ammonium carbonate using a plastic dropping pipette. The gel was left in the ammonium carbonate for 2 hours, then separated off and rinsed, air-dried, washed and oven-dried in the manner described for Example 1.
  • the overall porosity of the product was 4.16cc/g and the pore volume between 0.5 and 10 ⁇ m was 2.2cc/g.
  • the product contained 1.7wt% carbon.
  • the overall porosity of the product was 3.18cc/g and the pore volume between l and 10 ⁇ m was 2.0cc/g.
  • the product contained 2.8wt% carbon.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Organic Chemistry (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Silicon Compounds (AREA)
  • Catalysts (AREA)
  • Silicon Polymers (AREA)
  • Materials Applied To Surfaces To Minimize Adherence Of Mist Or Water (AREA)
  • Porous Artificial Stone Or Porous Ceramic Products (AREA)
  • Processing Or Creating Images (AREA)
  • Cosmetics (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)
EP19870309066 1986-10-16 1987-10-14 Wasserabweisende anorganische Produkte Expired - Lifetime EP0264268B1 (de)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT87309066T ATE76633T1 (de) 1986-10-16 1987-10-14 Wasserabweisende anorganische produkte.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB08624872A GB2199541A (en) 1986-10-16 1986-10-16 Production of engineering drawings
GB8624872 1986-10-16

Publications (3)

Publication Number Publication Date
EP0264268A2 true EP0264268A2 (de) 1988-04-20
EP0264268A3 EP0264268A3 (en) 1989-07-19
EP0264268B1 EP0264268B1 (de) 1992-05-27

Family

ID=10605875

Family Applications (1)

Application Number Title Priority Date Filing Date
EP19870309066 Expired - Lifetime EP0264268B1 (de) 1986-10-16 1987-10-14 Wasserabweisende anorganische Produkte

Country Status (11)

Country Link
US (1) US4888309A (de)
EP (1) EP0264268B1 (de)
JP (1) JPS63190774A (de)
AT (1) ATE76633T1 (de)
AU (1) AU602924B2 (de)
CA (1) CA1270498A (de)
DE (1) DE3779393D1 (de)
ES (1) ES2033320T3 (de)
GB (1) GB2199541A (de)
GR (1) GR3005514T3 (de)
ZA (1) ZA877796B (de)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4888309A (en) * 1986-10-16 1989-12-19 Unilever Patent Holdings Bv Hydrophobic, highly porous, three-dimensional inorganic structures
EP0360244A1 (de) * 1988-09-20 1990-03-28 Asahi Kogaku Kogyo Kabushiki Kaisha Poröser keramischer Sinter und Verfahren zu dessen Herstellung
GB2267486A (en) * 1992-06-02 1993-12-08 British Gas Plc Porous amorphous silica-alumina
US5871646A (en) * 1992-06-02 1999-02-16 British Gas Plc Porous amorphous silica-alumina refractory oxides, their preparation and use as separation membranes
ITUB20153550A1 (it) * 2015-09-11 2017-03-11 Signa Labs S R L Materiale, uso e metodo di realizzazione di tale materiale

Families Citing this family (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB8511048D0 (en) * 1985-05-01 1985-06-12 Unilever Plc Inorganic structures
GB9122481D0 (en) * 1991-10-23 1991-12-04 Roberts Robert G Method and apparatus for representing articles of furniture
EP0641290B1 (de) * 1992-05-20 1996-09-11 E.I. Du Pont De Nemours And Company Verfahren zur herstellung anorganischer gele
DK0711261T3 (da) * 1993-07-28 2002-08-12 Univ Monash Zirconiumoxidpartikler
JP2580537B2 (ja) * 1994-06-27 1997-02-12 工業技術院長 シリカ球状粒子からなる三次元網状構造体
DE19648798C2 (de) * 1996-11-26 1998-11-19 Hoechst Ag Verfahren zur Herstellung von organisch modifizierten Aerogelen durch Oberflächenmodifikation des wäßrigen Gels (ohne vorherigen Lösungsmitteltausch) und anschließender Trocknung
US6638885B1 (en) 1997-05-22 2003-10-28 The Trustees Of Princeton University Lyotropic liquid crystalline L3 phase silicated nanoporous monolithic composites and their production
US6048908A (en) 1997-06-27 2000-04-11 Biopore Corporation Hydrophilic polymeric material
US7002728B2 (en) 1997-08-28 2006-02-21 E Ink Corporation Electrophoretic particles, and processes for the production thereof
US7247379B2 (en) 1997-08-28 2007-07-24 E Ink Corporation Electrophoretic particles, and processes for the production thereof
EP1093486B1 (de) * 1998-06-05 2004-08-04 Cabot Corporation Nanoporöse interpenetrierende organisch-anorganische netzwerke
AU2002250304A1 (en) * 2001-03-13 2002-09-24 E Ink Corporation Apparatus for displaying drawings
US7230750B2 (en) 2001-05-15 2007-06-12 E Ink Corporation Electrophoretic media and processes for the production thereof
US6580545B2 (en) * 2001-04-19 2003-06-17 E Ink Corporation Electrochromic-nanoparticle displays
WO2002093246A1 (en) * 2001-05-15 2002-11-21 E Ink Corporation Electrophoretic particles
ITTO20120753A1 (it) 2012-08-30 2014-03-01 St Microelectronics Srl Dispositivo incapsulato esposto all'aria ambiente e a liquidi e relativo processo di fabbricazione
WO2017214531A1 (en) 2016-06-10 2017-12-14 Chevron U.S.A. Inc. Hydrophobic adsorbents and mercury removal processes therewith
FR3065649B1 (fr) 2017-04-28 2020-05-29 IFP Energies Nouvelles Monolithe poreux contenant du tio2 et son procede de preparation
FR3065651B1 (fr) 2017-04-28 2020-05-29 IFP Energies Nouvelles Procede de preparation d'un monolithe a porosite multimodale
RU2769341C2 (ru) * 2017-06-15 2022-03-30 СЭСОЛ (ЮЭсЭй) КОРПОРЕЙШН Гидрофобные поверхностно модифицированные оксиды алюминия и способ их получения

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Publication number Priority date Publication date Assignee Title
FR1326386A (fr) * 1962-01-30 1963-05-10 Pechiney Saint Gobain Nouveaux produits poreux à base d'alumine
US3301635A (en) * 1965-07-01 1967-01-31 Du Pont Molded amorphous silica bodies and molding powders for manufacture of same
FR1583791A (de) * 1968-03-29 1969-12-05
DE2155045B2 (de) * 1971-11-05 1976-05-06 Sebestian, Imrich, Dr., 6000 Frankfurt; Halasz, Istvan, Prof. Dr., 6600 Saarbrücken Verfahren zur herstellung von kugelfoermigen poroesen sio tief 2-teilchen
US3892580A (en) * 1973-03-26 1975-07-01 Corning Glass Works Method of making porous inorganic bodies
JPS51115298A (en) * 1975-04-03 1976-10-09 Agency Of Ind Science & Technol Process for production of spherical silica gel
US4011096A (en) * 1975-06-10 1977-03-08 E. I. Du Pont De Nemours And Company Vesiculated silica microspheres
US4190457A (en) * 1978-06-09 1980-02-26 Phillips Petroleum Co. Preparation of inorganic xerogels
DE3151374A1 (de) * 1981-12-24 1983-07-14 Bayer Ag, 5090 Leverkusen Waessrige zubereitung und ihre verwendung bei der herstellung keramischer massen
NL8402158A (nl) * 1983-07-09 1985-02-01 Sumitomo Cement Co Poreus keramisch materiaal en werkwijze voor de bereiding daarvan.
GB8511048D0 (en) * 1985-05-01 1985-06-12 Unilever Plc Inorganic structures
GB2199541A (en) * 1986-10-16 1988-07-13 Rig Design Services Production of engineering drawings

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4888309A (en) * 1986-10-16 1989-12-19 Unilever Patent Holdings Bv Hydrophobic, highly porous, three-dimensional inorganic structures
EP0360244A1 (de) * 1988-09-20 1990-03-28 Asahi Kogaku Kogyo Kabushiki Kaisha Poröser keramischer Sinter und Verfahren zu dessen Herstellung
US5171720A (en) * 1988-09-20 1992-12-15 Asahi Kogaku Kogyo K.K. Porous ceramic sinter and process for producing same
GB2267486A (en) * 1992-06-02 1993-12-08 British Gas Plc Porous amorphous silica-alumina
GB2267486B (en) * 1992-06-02 1996-02-14 British Gas Plc Porous amorphous silica-alumina refractory oxides, their preparation and use as separation membranes
US5871646A (en) * 1992-06-02 1999-02-16 British Gas Plc Porous amorphous silica-alumina refractory oxides, their preparation and use as separation membranes
US6042727A (en) * 1992-06-02 2000-03-28 British Gas Plc Porous amorphous silica-alumina refractory oxides, their preparation and use as separation membranes
ITUB20153550A1 (it) * 2015-09-11 2017-03-11 Signa Labs S R L Materiale, uso e metodo di realizzazione di tale materiale
WO2017042727A1 (en) * 2015-09-11 2017-03-16 Signa Labs S.R.L. Material, use thereof and method to manufacture said material
CN108025977A (zh) * 2015-09-11 2018-05-11 西格纳实验室有限公司 材料、其用途和制造所述材料的方法
US10730797B2 (en) 2015-09-11 2020-08-04 Signa Labs S.R.L. Material, use thereof and method to manufacture said material

Also Published As

Publication number Publication date
GB2199541A (en) 1988-07-13
ES2033320T3 (es) 1993-03-16
AU7959587A (en) 1988-04-21
US4888309A (en) 1989-12-19
JPS63190774A (ja) 1988-08-08
AU602924B2 (en) 1990-11-01
EP0264268A3 (en) 1989-07-19
DE3779393D1 (de) 1992-07-02
ATE76633T1 (de) 1992-06-15
GB8624872D0 (en) 1986-11-19
CA1270498A (en) 1990-06-19
EP0264268B1 (de) 1992-05-27
ZA877796B (en) 1989-06-28
GR3005514T3 (de) 1993-06-07

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